|Publication number||US4089765 A|
|Application number||US 05/532,696|
|Publication date||May 16, 1978|
|Filing date||Dec 13, 1974|
|Priority date||Dec 14, 1973|
|Also published as||CA1001994A, CA1001994A1|
|Publication number||05532696, 532696, US 4089765 A, US 4089765A, US-A-4089765, US4089765 A, US4089765A|
|Inventors||Michael A. Dudley|
|Original Assignee||Canada Wire And Cable Limited|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (8), Referenced by (33), Classifications (6), Legal Events (2)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This invention relates to electroimpregnation of paper and non-woven fabrics with ionic materials.
Several methods of coating or modifying paper or non-woven fabrics are used for various applications. Some of these known methods make use of a doctor-blade spread latex to improve wet rub resistance such as disclosed in French Pat. No. 1,516,761, or of a roller coated solution for the manufacture of release paper as disclosed in U.S. Pat. No. 3,403,045, or of an electrostatic spray to produce paper dish cloths as disclosed in U.S. Pat. No. 3,484,275. Melt extrusion is also used to make release paper as disclosed in German Pat. No. 1,936,001. Still another known method uses graft polymerization for making insulating paper.
Electrodeposition, which has recently evolved into a common technical method for forming protective and decorating coatings on metal surfaces, has also been experienced for depositing onto paper or non-woven fabrics materials dispersed as a suspension into a liquid as disclosed in Canadian Pat. No. 781,420. However, to applicant's knowledge, electrical methods have never been used to impregnate paper or non-woven fabrics having a predetermined degree of porosity with true solutions of materials.
It is therefore the object of the present invention to impregnate paper or non-woven fabrics with ionically charged materials in solution. That is, the materials in solution exist in dissociated states so as to form ionic solutions.
The process, in accordance with the invention, comprises the step of forming an aqueous solution containing about 1 to 30% of an ionic material having a specific conductance lower than 0.003 mhos cm-1 in a bath provided with cathode and anode electrodes submerged in the solution, introducing a sheet of paper or non-woven fabric into the bath in contact with the cathode or anode electrode, dependent on the polarity of the ionic material, and applying a predetermined DC voltage to the electrodes so as to cause the ions of such material to impregnate the paper or non-woven fabric as the ions move toward one or the other of the electrodes and deposit within the paper or non-woven fabric as partially or totally associated molecules.
The paper or non-woven fabric may be prewetted to impart thereto a predetermined moisture content so as to prevent excessive buckling of the sheet of paper or non-woven fabric upon immersion into the solution.
It has been found experimentally that the above method may advantageously be used to impregnate paper or non-woven fabric with a polymeric material to improve its dielectric strength and moisture absorption resistance characteristics for use in various electrical applications such as the manufacture of cables and transformers.
After impregnation, the sheet of paper or non-woven fabric may be rinsed to remove surface material prior to drying and/or curing.
The above method has also been successfully used for the impregnation of paper with ionic sizes and dyes for the paper industry. The present in-line sizing operation consists of passing the paper through a puddle of size solution, which is maintained in the nip of two rolls. Sizes include glues, carboxy methyl cellulose and ionic starches. Starches which are used to improve the writing and printing qualities of paper are presently applied at 5 to 10% total solids, with a viscosity of 15-50 centipoise at 140° F, to ensure total impregnation. Papermakers would like to use high concentrations or to go to higher viscosity starches such as 100 centipoise. Experiments have proven that a higher percentage of starch may be impregnated in paper using the electroimpregnation method in accordance with the invention. In practice, the two nip rolls on each side of the paper could be used as the anode and cathode electrodes.
At the present time, only 50% of the dyes used in papermaking can be applied at the size press because of uneven impregnation due to the short residence time of the paper in the nip rolls. Here again, it has been found that electroimpregnation in accordance with the present invention can improve the quality and of the speed of the dyeing operation. Although it has been found that, due to the pH variation of the solution at the surface of the paper during the electroimpregnation, there may be slight changes in the color of the dye, this is not critical and may be controlled.
The invention will now be disclosed with reference to various applications thereof which are disclosed by way of example only with no intention to limit the scope thereof.
A number of tests were made to electroimpregnate paper with a polymeric material. The laboratory apparatus used for electroimpregnation was a cubic glass cell 3.50 inch square filled with an electroimpregnating solution of polymeric material. Two, free moving, 3 inch square stainless steel electrodes were positioned in the glass cell and mounted in polymethyl methacrylate carriers with only one face exposed to the electroimpregnating solution. Various paper samples were prewetted with distilled water to prevent excessive buckling upon immersion into the solution, smoothed onto the anode to remove air bubbles, and taped to the anode around the edges to prevent the deposition of the polymeric material on the anode other than by passage of the solution through the paper samples. After impregnation, the samples were rinsed in distilled water and cured. The cure time was initially set at 4 minutes at 180° C, but was later standardized to 15 minutes at 150° C to eliminate the possibility of charring the paper. It is to be understood that the cure time and temperature may vary depending on the polymeric solution.
The polymeric solution may contain from 1 to 30% resin with the preferable range being 5 to 15%. The resin may be anionic or cationic in nature. The experimental resin used was an epoxy/ester water soluble resin, although any electroimpregnatable synthetic polycarboxylic acid resin, which include epoxy/ester, alkyd, acrylic and polyester resin, can be used.
The paper samples used were "electrical" grades, that is papers in which the incidence of ionic species, which may cause surface deposition of the resin, is very low. Such samples included 0.003 inch thick manilla papers and nitrogen containing heat-resistant papers known in the trade as "Insuldur" and having a thickness of 0.003 to 0.005 inch. The porosity of the paper used is important. Under the laboratory conditions, a paper having a densometer value of 300-400 seconds could be impregnated only to a thickness of 0.005 inch.
Each paper sample, after impregnation and cure, was tested for dielectric breakdown voltage and moisture absorption characteristics. The dielectric breakdown voltage was tested by the Westinghouse method (Westinghouse Electric Corporation, PD Specification 42355 AP through AT Revision J, 1968) which uses a pair of two-inch diameter plate electrodes, connected to a usual voltage tester. The moisture absorpotion was evaluated by exposing pre-dried two-inch diameter impregnated paper samples to 100% relative humidity for 24 hours, and determining the weight gain immediately after removal. The pre-dried sample weight was obtained after exposing the samples to 150° for 15 minutes, and cooling in a desiccator before weighing.
The electroimpregnation may be carried out using substantially constant voltage or constant current. The voltage, current and duration of power required for impregnation are dependent on several factors, namely the electrode separation, the paper porosity and the paper thickness as it will be seen in the following Tables 1 and 2. Electrode separation is the most important variable when using constant voltage, separations of 1.0 to 2.5 inches having been used successfully. The epoxy/ester resin used was the commercially available epoxy resin Epon 1001 (marketed by Shell Chemical Company Limited), derived from epichlorohydrin and bisphenol-A, and esterified with dehydrated castor oil fatty acids to produce an epoxy/ester with an acid value (m.g. potassium hydroxide per gram of resin) of from about 8 to 10, and subsequently heated with succinic anhydride until the acid value reaches about 50. Such an epoxy/ester water soluble resin is more clearly described in U.S. Pat. No. 3,736,276 granted May 29, 1973.
TABLE 1__________________________________________________________________________ELECTROIMPREGNATION OF PAPER USING CONSTANT VOLTAGEAND AN EPOXY/ESTER WATER SOLUBLE RESIN Dielectric % MoistureElectrode Applied Breakdown AbsorptionSepara- Voltage, Time Voltage 24 hours atPapertion in. V sec. V 100% R.H.__________________________________________________________________________Insuldur1.0 100 5.12 900 5.10.003-in.1.0 125 5.04 900 4.41.0 150 5.36 1100 5.81.5 100 5.19 900 4.11.5 125 4.88 900 4.51.5 150 5.20 900 12.12.5 100 5.20 900 4.52.5 125 5.04 900 9.12.5 150 5.27 900 16.9Control -- -- 750 12.0Insuldur1.0 100 5.27 1250 4.50.005-in.1.0 125 5.03 1300 5.71.0 150 5.27 1350 5.11.5 100 4.96 1250 4.51.5 125 5.04 1450 5.51.5 150 5.12 1800 5.22.5 100 5.04 1250 1.92.5 125 5.19 1450 3.72.5 150 5.19 1550 3.5Control -- -- 1100 13.0__________________________________________________________________________
TABLE 2__________________________________________________________________________ELECTROIMPREGNATION OF PAPER USING CONSTANT CURRENTAND AN EPOXY/ESTER WATER SOLUBLE RESIN Dielectric % MoistureElectrode Breakdown AbsorptionSeparation, Current, Time, Voltage 24 hours atPaperin. amps sec. V 100% R.H.__________________________________________________________________________Insuldur1.0 0.2 20.25 1250 2.80.003-in.1.0 0.3 10.10 1200 8.11.0 0.4 10.40 1450 9.31.0 0.5 10.72 1250 5.21.0 1.0 5.27 1250 6.01.5 0.2 10.55 900 12.81.5 0.3 10.25 1000 7.21.5 0.4 10.25 1000 11.51.5 0.5 10.15 1250 6.12.5 0.3 10.10 1250 6.12.5 0.4 10.32 1250 5.82.5 0.5 10.48 1200 8.8Control -- -- 750 20.5Insuldur1.0 0.3 10.0 1350 9.30.005-in.1.0 0.5 10.15 1400 6.31.0 0.6 10.37 1400 5.51.0 0.7 10.40 1450 5.21.5 0.4 10.15 1300 7.51.5 0.5 10.07 1350 4.81.5 0.6 10.30 1300 3.11.5 0.7 10.07 1350 4.52.5 0.3 9.92 1300 8.22.5 0.4 9.70 1300 4.22.5 0.5 10.30 1300 4.82.5 0.6 10.55 1250 4.32.5 0.7 10.45 1400 3.2Control -- -- 1100 22.5__________________________________________________________________________
Under the experimental conditions used in the above Tables, average dielectric breakdown voltage improvements of about 55% and 80% were achieved using constant voltage and constant current control respectively. Reduction in moisture absorption was about 70% and 80% using constant voltage and constant current control respectively.
The above disclosed method produces a polymer impregnated paper suitable for electrical insulation applications and which obviates the vacuum drying step in the cable making. Such a polymer impregnated paper may be used, without oil impregnation, for cable insulation.
The above paper impregnation method has also been successfully used for impregnating a 0.004 inch thick non-woven fabric, having a porosity of 300 cfm/sq.ft., with a 5% anionic electrocoating solution of an acrylic resin known under the trademark Baycryl W-460 sold by Bayer Germany. The results of this test are illustrated in the following Table:
TABLE 3______________________________________ % Moisture DielectricElectrode Applied Absorption BreakdownSeparation Voltage Time after 24 hrs. Voltagein. V Seconds at 100% R.H. V______________________________________1.0 50 10 9.9 9501.0 75 10 16.2 1,3401.0 100 10 2.4 1,1501.0 125 10 10.9 1,300Control 18.5 1,000______________________________________
The results illustrated in the above table show the improvements experienced in the dielectric strength and moisture absorption resistance characteristics of the non-woven fabric.
Various experiments have also been carried out using electroimpregnating solutions containing ionic sizes and dyes. For example, electroimpregnation of a 0.019 inch thick Bond paper, taken from a paper machine prior to entering the size press, was carried out using a 10% solution of a cationic starch known under the trade name Catobond 60. The results of the above experiment are illustrated in the following Table:
TABLE 4______________________________________ Ap- Elec- plied Dip trode Vol- wt. pickupPaper Time, Separa- tage on 2" dia.Treatment sec. tion, in. V circle, mg______________________________________Dry paper, dipped 1.5 -- -- 1.5into starch solutionDry paper, electro- 1.5 3.0 150 8.1impregnated with starchPrewetted paper, dipped 1.5 -- -- 0.9into starch solutionPrewetted paper, electro- 1.5 3.0 150 9.5impregnated with starch______________________________________
It will be seen from the above Table that the weight of starch picked up by the paper electroimpregnated with starch is between 5 and 10 times the corresponding weight of starch picked up by paper which is simply dipped into a starch solution.
Electroimpregnation of 0.019 inch thick Bond paper, taken from a paper machine prior to entering the size press, has been carried out with a 1% aqueous solution having 2.5% butyl cellosolve as a coupling solvent, of a cationic dye known under the trade name Chrysoidine Y having the following formula: ##STR1##
The results of the above experiment are illustrated in the following Table:
TABLE 5______________________________________ Ap- Elec- plied Dip trode Vol- Wt. pickupPaper Time, Separa- tage on 2" dia.Treatment sec. tion, in. V circle, mg______________________________________Prewetted paper, 1.0 -- -- 1.5dipped into dye 30.0 -- -- 1.9solutionPrewetted paper, 1.0 1.5 100 3.7electroimpregnated 30.0 1.5 100 16.6with dye______________________________________
In the electroimpregnation Tables 4 and 5, the cathode with either the dry or prewetted paper attached was dipped into the respective solutions with the applied voltage on in order to reproduce the conditions of the straight dip comparisons.
In carrying out electroimpregnation of dyes, sizes and polymeric materials, it became apparent that paper porosity was not a factor upon which a range could be set. It is believed to be obvious to a man skilled in the art to choose a paper or a non-woven fabric of a porosity such as to permit impregnation of the paper or non-woven fabric. However, it is important that to obtain suitable electroimpregnation the specific conductance of the solution, whether dye, size, or polymeric material should be less than 0.003 mhos cm-1. It was found that impregnation rate is very low or negligible above that value. The preferred range is from 0.0005 to 0.0015 mhos cm-1.
The degree of impregnation is dependent on the molecular weight of the ionic material (ionic starch, resin or dye) and the charge/weight ratio of the ionic material plus the degree of porosity of the paper or non-woven fabric to be impregnated. The lower the molecular weight, the easier the impregnation. Similarly, the higher the charge/weight ratio, the greater is the impregnation. Finally, the higher the porosity the greater is the impregnation.
It is to be understood that the above disclosed impregnation method could be carried out on a continuous basis by impregnating paper at the "wet end" of a paper production line, resulting in both capital equipment and processing cost savings.
Although the invention has been disclosed with reference to electroimpregnation of paper and non-woven fabrics with ionic polymeric materials, ionic sizes and ionic dyes, it is to be understood that it could also be used for the impregnation of paper and non-woven fabrics with other materials such as fire retardants, and also for polymeric transparentizing of paper.
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|U.S. Classification||204/507, 162/184, 162/192|
|Jul 24, 1991||AS||Assignment|
Owner name: 555794 ONTARIO INC.
Free format text: CHANGE OF NAME;ASSIGNOR:CANADA WIRE AND CABLE LIMITED (CHANGED INTO);REEL/FRAME:005784/0544
Effective date: 19871213
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Effective date: 19871231
Owner name: NORANDA MANUFACTURING INC.
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Effective date: 19910716
|Jan 15, 1993||AS||Assignment|
Owner name: ALCATEL CANADA WIRE INC., CANADA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:NORANDA INC.;REEL/FRAME:006388/0059
Effective date: 19920901